Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Water | HCID 962 | — |
| Reactant | 2-(Hydroxymethyl)-2-methylpentanal | HCID 12499071 | — |
| Solvent | Methanol | HCID 887 | — |
| Product | 2-Methylpentaldehyde | HCID 31245 | — |
| Product | 2-Methyl-2-propylpropane-1,3-diol | HCID 66220 | — |
| Product | 2-(Hydroxymethyl)-2-methylpentanal | HCID 12499071 | — |
Reaction Steps
Using the method described in Example 1(b), one part per hour of a 72 percent strength by weight aqueous solution of 2-methyl-2-propyl-3-hydroxypropanal is hydrogenated, over the catalyst prepared as described in Example 1(a), at 130° C. and 30 bar, with a throughput of 0.36 part of 2-methyl-2-propyl-3-hydroxypropanal per liter of catalyst per hour. The conversion is 89.5 percent. The hydrogenated material is fractionated through a packed column. After first runnings of water and small amounts of methanol, 2-methylpentanal and 2-methyl-2-propyl-3-hydroxypropanal, 2-methyl-2-propyl-propane-1,3-diol, of boiling point 112°-113° C./5 mbar (melting point 58°-60° C.), is obtained in an amount corresponding to 0.6967 part per hour. This is equivalent to a yield of 95.3% of theory, based on starting material.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04393251 |
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| Source dataset | uspto-grants-1983_07 |
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| ORD ID | ord-abb5b6632e174632b7299241205e147d |
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| Source note | uspto-grants-1983_07 |
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